In this paper, we propose to study the dynamics of fixed bed reactors with axial dispersion in the general case of a non-isothermal process involving N components and M reactions. It will be shown by using singular perturbation that for large dispersion coefficient values, the fixed bed reactor tends to a stirred tank reactor. Singular perturbation results in a series expansion of the state variables (component concentrations and temperature). The computation will be carried out up to the first order. The dynamical equations of the zero order approximation are the those of the corresponding stirred tank reactor
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...
Heterogeneous and pseudo-homogeneous dynamic models, for fixed bed catalytic reactors are presented ...
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...
In this paper, we propose to study the dynamics of fixed bed reactors with axial dispersion in the g...
A methodology for studying a multicomponent catalytic fixed bed reactor having a significant axial d...
We study axial heat and mass transfer in a highly diffusive tubular chemical reactor in which a simp...
In this paper a mathematical study is made of the effect of dispersion on the optimum residence time...
This work is a mathematical study of the effect of dispersion on the optimum residence times of seve...
This paper deals with the dynamical properties (observability, reachability, stabilizability, detect...
The singularity theory and continuation techniques are combined to classify the static and dynamic b...
The long performance of an isothermal fixed bed reactor undergoing catalyst poisoning is theoretical...
The singularity theory and continuation techniques are combined to classify the static and dynamic b...
Various problems regarding the behaviour of fixed bed catalytic reactors involving highly exothermic...
This paper is dedicated to the dynamical analysis of tubular reactor models, namely plug-flow and ax...
Abstract-A mathematical model for the startup period of a fixed-bed reactor with first-order reactio...
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...
Heterogeneous and pseudo-homogeneous dynamic models, for fixed bed catalytic reactors are presented ...
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...
In this paper, we propose to study the dynamics of fixed bed reactors with axial dispersion in the g...
A methodology for studying a multicomponent catalytic fixed bed reactor having a significant axial d...
We study axial heat and mass transfer in a highly diffusive tubular chemical reactor in which a simp...
In this paper a mathematical study is made of the effect of dispersion on the optimum residence time...
This work is a mathematical study of the effect of dispersion on the optimum residence times of seve...
This paper deals with the dynamical properties (observability, reachability, stabilizability, detect...
The singularity theory and continuation techniques are combined to classify the static and dynamic b...
The long performance of an isothermal fixed bed reactor undergoing catalyst poisoning is theoretical...
The singularity theory and continuation techniques are combined to classify the static and dynamic b...
Various problems regarding the behaviour of fixed bed catalytic reactors involving highly exothermic...
This paper is dedicated to the dynamical analysis of tubular reactor models, namely plug-flow and ax...
Abstract-A mathematical model for the startup period of a fixed-bed reactor with first-order reactio...
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...
Heterogeneous and pseudo-homogeneous dynamic models, for fixed bed catalytic reactors are presented ...
Modeling of evaporative separators with mass and energy balances, only, often leads to di erential a...